Synthesis of higher polyol fatty acid polyesters by transesterification

Inactive Publication Date: 2003-01-07
THE PROCTER & GAMBLE COMPANY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

It has now been found that higher sucrose polyesters can be produced without the use of lower alkyl ester intermediates or methyl carbitol by transesterification of sucrose by triglyceride. Glycerine, mono- and/or di-glycerides, the by-products of the reaction, are derived from the triglyceride when at least one ester group of the triglyceride has been transferred to sucrose. Removal of glycerine, mono- and/or di-glycerides drives the reaction to high degrees of esterification, and polyol penta-to octa-esters are formed. The need to produce fatty acid lower alkyl esters in a separate step and the need

Problems solved by technology

Unfortunately, the need to synthesize fatty acid lower alkyl ester intermediates increases the operating costs of the polyol polyester synthetic process, and the reaction of polyol and fatty acid lower alkyl ester results in the production of lower alkyl alcohol as a by-product.
Systems for the capture of lower alkyl alcohol are required, and the need to separate and handle the lower alkyl alcohol increases the risk of discharges of alcohol into the environment.
Unfortunately, methyl carbitol is relatively toxic and would be unsuitable for use in food grade polyol polyester production.
Parker et al.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 2

Step (1): Sucrose (35 g) and 543 g of high oleic sunflower oil triglyceride are mixed in about a 6:1 molar ratio and solubilized in 525 ml of dimethylformamide (DMF). Potassium carbonate (3 g) is added.

Step (2): The mixture is reacted for about 65 minutes at 120.degree. C. (248.degree. F.) at atmospheric pressure; the DMF is then removed by distillation. At the end of Step (2) the mixture comprises about:

Steps (3) and (4): Sodium methoxide (0.3 g) is added to 300 g of the material produced in Step (2). The mixture is reacted further for about 76 hours at 150-230.degree. C. (302-446.degree. F.), and 60.times.10.sup.-3 mm Hg to 20.times.10.sup.-3 mm Hg. Fluid is recirculated through a thin film evaporator. Glycerine and mono- and di-glycerides are simultaneously removed. The process results in the formation of highly esterified sucrose esters (about 70% of the sucrose polyesters were octa-esters).

The remaining reaction mixture comprises about:

The mixture comprises no monoglycerides or...

example 3

Steps (1) and (2): Sucrose ester feed material is produced by transesterification of soybean methyl esters with sucrose. The crude material is washed, dried under vacuum, bleached with silica gel, and filtered. The excess methyl esters are removed on a wiped film evaporator. The sucrose ester feed material composition is about:

Steps (3) and (4): The sucrose ester feed material (6580 g) and 4770 g of triglycerides from a corn / canola oil blend are mixed. Catalyst, 55 g of 25% sodium methoxide in methanol, is added.

The mixture is reacted at a temperature of about 225.degree. C. (437.degree. F.) and a pressure of about 2.times.10.sup.-3 mm Hg to about 4.times.10.sup.-3 mm Hg. The mix is passed 41 times through a molecular still. The total residence time of the passes is about 6 minutes.

Short path distillation is utilized to remove the transesterification reaction by-products. A wiped film evaporator with an internal condenser is used.

The process results in the formation of highly esteri...

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Abstract

A process for synthesizing polyol fatty acid polyesters comprising the steps of (1) mixing ingredients comprising (a) unesterified first polyol having hydroxyl groups, (b) second polyol esterified with fatty acids, (c) basic catalyst, and (d) emulsifying agent to form a mixture of ingredients; (2) reacting the mixture of ingredients at a temperature sufficient to obtain a transesterification reaction products and by-products; and (3) removing at least a portion of the by-products from the transesterification reaction mixture; and (4) further heating the transesterification reaction products and ingredients from step (3) at a temperature and for a time sufficient to esterify at least about 50% of the hydroxyl groups of the first polyol.

Description

This invention relates to processes for the production of polyol fatty acid polyesters, which processes eliminate the need to synthesize and purify lower alkyl ester intermediates. More particularly, this invention relates to processes for synthesizing polyol fatty acid higher polyesters by reaction of unesterified polyol, preferably selected from the group consisting of monosaccharides, disaccharides, polysaccharides, sugar alcohols, sugar ethers, polyglycerols and polyalkoxylated glycerols, and a second polyol esterified with fatty acids and selected from monoglycerides, diglycerides and triglycerides.The food industry has recently focused attention on polyol polyesters for use as low-calorie fats in food products. Triglycerides (triacylglycerols) constitute about 90% of the total fat consumed in the average diet. One method by which the caloric value of edible fat can be lowered is to decrease the amount of triglycerides that is consumed, since the usual edible triglyceride fats ...

Claims

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Application Information

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IPC IPC(8): C07H13/06C07H13/00C07C67/03C07C69/52
CPCC07C67/03C07H13/06C07C69/52
Inventor TROUT, JAMES EARLSCHAFERMEYER, RICHARD GERARD
Owner THE PROCTER & GAMBLE COMPANY
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